In the commercial chloride process, titanium is extracted from Ti concentra
tes at high temperatures (800-1,500 degreesC), and the high-purity rutile i
s the primary raw material. Chlorination at high temperatures results in hi
gh-energy consumption, rapid corrosion of equipment pipelines and control s
ystem, and agglomeration of the solid bed by the liquid byproducts. The hig
h-purity rutile is expensive and its natural deposit is being depleted. The
refore, a low-temperature Ti extraction process using Ti-waste as the prima
ry raw material is highly desirable. Thermodynamic equilibrium simulation o
f the reaction system shows that the extraction of Ti from Ti waste is feas
ible at a temperature as low as 200 degreesC. In this study, a simple techn
ology was used to remove diffusion barriers, and a low-temperature chloride
process was developed. The chlorination reaction operates at 300 - 350 deg
reesC, and Ti-waste can be used to replace the expensive rutile. Up to 80%
of the titanium can be recycled in 5 min at 350 degreesC. The extraction of
other components has a relatively low extent, so a selective extraction of
Ti can be achieved. A fluidized-bed reactor was used for the chlorination
process. The formation of an activated TiO2-C-Cl complex on the TiO2/C inte
rface accounts for the gas-solid-solid reaction mechanism.